CN204356134U - A kind of upward flowing type BAF - Google Patents
A kind of upward flowing type BAF Download PDFInfo
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- CN204356134U CN204356134U CN201420784793.6U CN201420784793U CN204356134U CN 204356134 U CN204356134 U CN 204356134U CN 201420784793 U CN201420784793 U CN 201420784793U CN 204356134 U CN204356134 U CN 204356134U
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- filter tank
- filter
- inhalant region
- filtrating area
- dividing plate
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
The utility model relates to a kind of upward flowing type BAF, and this BAF comprises several filter tanks of connecting successively; Any one filter tank is equipped with inhalant region, and sewage enters the inhalant region bottom first filter tank by pipeline, and inhalant region is also connected with shore pipe; Any one filter tank is all provided with filtrating area in the upside of inhalant region, and filtrating area is abound with ceramic grain filter, and the downside of filtrating area is provided with support dividing plate, and dividing plate is installed with filter, is also provided with aeration tube in the downside of filtrate; Except first filter tank, any one filter tank near on the top of side, a filter tank be equipped with overfalling weir, and the inhalant region in any one filter tank is all connected by hydraulic pipe with the overfalling weir in this grade of filter tank, the height of the overfalling weir in this multiple filter tank reduces to side, water side gradually from feed-water end side of the present utility model.The utility model is easy to safeguard, not easily block and the developing result that effectively improve sewage.
Description
Technical field
The utility model belongs to technical field of sewage, is specifically related to a kind of upward flowing type BAF.
Background technology
BAF (Biological Aerated Filter, BAF) is the external popularization that begins one's study from the eighties, to the new wastewater treatment method that the initial stage nineties has been mature on the whole.Its ultimate principle is on coagulation basis, with the microbial film of granular filter material and apposition growth thereof for treatment media, give full play to the multistage predation of food in biological metabolism effect, physical filtering effect, the physisorption of film and film and filtrate and reactor, realize pollutent and remove in same unitary reactor.There is different aerobic, anoxic zones in reactor, can synchronously realize nitrated, denitrification, while organics removal, reach the object of denitrogenation.
What integrate biomembranous Strong oxdiative degradation capability and filtering layer due to BAF retains usefulness, there is the advantages such as Chi Rong little, effluent characteristics is high, flow process is simple, be widely used at present the pre-treatment of the process of municipal effluent, Treated sewage reusing and slightly-polluted raw water, become a kind of economical, sewage second-level, tertiary treatment process efficiently.It can remove SS, COD, BOD, nitrated denitrogenation, denitrification dephosphorization etc.
But BAF of the prior art operationally, due to head loss, is intake at filtrating area reduced velocity flow, is easily caused inhalant region collection mud, blocking filtrate and filter, thus affect the Degradation increase filtrate cost of microbial film to waste water.
Therefore, a kind of easy care, not easily blocking is provided and the BAF effectively improving developing result becomes the technical problem that those skilled in the art need solution badly.
Utility model content
For above-mentioned deficiency, the technical problems to be solved in the utility model is to provide a kind of easy care, not easily blocking and effectively improves a kind of upward flowing type BAF of developing result.
To achieve these goals, the utility model is achieved through the following technical solutions:
A kind of upward flowing type BAF, this BAF comprises several filter tanks of connecting successively, is provided with filtrating area and inhalant region from top to bottom in any one filter tank;
Described inhalant region is connected with sewage water inlet pipe, and sewage water inlet pipe is provided with wastewater influent tube valve, and described inhalant region is also connected with shore pipe, and described mud line is provided with spoil disposal valve and sludge pump;
Be abound with the biofilter material of haydite shape in described filtrating area, the downside of filtrating area is provided with support dividing plate, dividing plate is evenly equipped with the through hole penetrating plate body, and described through hole is installed with filter; This filter tank also in the upside of dividing plate, the downside of biofilter material is provided with aeration tube, the pipe shaft of described aeration tube is provided with solarization air cap;
Except first filter tank, any one filter tank is equipped with overfalling weir at the top near side, upper level filter tank, and the inhalant region in any one filter tank is all connected by hydraulic pipe with the overfalling weir in this filter tank; The height of the overfalling weir in this multiple filter tank reduces to side, water side gradually from feed-water end side.
Preferably, the upside of described filtrating area is provided with baffle plate, and described baffle plate offers flowing hole.
Preferably, described filter tank, dividing plate and baffle plate are skeleton construction.
The beneficial effects of the utility model are:
1), the utility model takes the filter type of upward flow, namely upwards flowed with the air being entered inhalant region by aeration tube is all parallel by the sewage entering inhalant region in waste pipe, thus while aeration, biofilter material is stirred, this filter type makes filtrate be in flow state all the time, efficiently avoid hardening and the short flow problem of sewage of filtrate; Meanwhile, in aqueous vapor uphill process, the ss suspended solid that bottom retains can be brought into middle and upper part, filter tank, add the water environment capacity in filter tank, extend the working hour in filter tank.
In addition, the turbulent fluctuation homogenizing that the aeration continued produces is conducive to the homogeneity of water distribution, when sewage flows through filter material layer from bottom to top, organic pollutant in microbial film absorption sewage is as himself metabolic nutritive substance, and under the condition of aeration oxygen supply is provided in filter material layer bottom, make the organism in waste water obtain aerobic degradation, and carry out nitrated denitrogenation, reach good filter effect.
Aerated conduit is arranged on inside, filtrating area by the utility model, whole filtrating area is divided into aerobic and anoxic two regions by aerated conduit, the nitration reaction of organic oxidative degradation and ammonia nitrogen in sewage fully can be realized in aerobic zone, in oxygen-starved area owing to there being part water to reflux under the barrier effect of upper strata baffle plate, the water of this partial reflux then realizes denitrification with the organic substrates that inputs in water inlet, thus greatly improves the treatment effect of sewage.
2), sewage in the utility model is when by filter material layer, pollutent in sewage is retained by filter material layer, and transformed by the biological degradation that filtrate adheres to, simultaneously, organism and the predetermined substance of dissolved state are also removed, along with the carrying out of filtering, the biomass newly produced due to filter material surface gets more and more, the ss suspended solid retained constantly increases, when solid matter accumulation acquires a certain degree, pile up and form mud and to be retained in filtering layer and to precipitate, and only allow the water after purifying pass through, biological treatment completely can be reached like this and need second pond be set in downstream and carries out sludge settling in a BAF.
When the mud in filtrating area reaches setting degree, the spoil disposal valve on mud line can be opened to filtrating area, start sludge pump, after forcing the mud gathered in discharge inhalant region, close spoil disposal valve again, adopt and greatly can shorten backwashing time in this way, increase aquifer yield, reduce and filter cost and effectively improve backwash effect.
3), the utility model is provided with the concrete baffle plate with flowing hole above filtrating area, thus in the decontamination process of sewage, effectively can prevent from taking away filtrate while discharge water purification above filtrating area, cause filterins media run-off and affect filter effect.
4), the utility model is also provided with the overfalling weir making the process current direction adjacent downstream filter tank of overflowing from upper end, filter tank, upstream, overfalling weir is provided with the hydraulic pipe leading to inhalant region, filter tank, and the height of overfalling weir in multiple filter tank reduces to side, water side gradually from feed-water end side of the present utility model.This frame mode, not only add the main-process stream of the sewage entered in this BAF, extend biological degradation interception and the filtration time of sewage, improve treatment effect, and the whole process of sewage is in the effect of water body gravity dirty voluntarily, energy consumption is lower, embodies the technical scheme of environmental protection further.
5) filtering basin, dividing plate and baffle plate, in the utility model are skeleton construction, are easy to cast in situs, and corrosion resistance and good, ensure that the operation that this BAF can be stable for a long time.
Accompanying drawing explanation
Below in conjunction with accompanying drawing and example, the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation setting up back-purge system in the utility model.
Fig. 3 is the structural representation of dividing plate.
Fig. 4 is the scheme of installation of filter.
The implication marked in figure is as follows:
1-filter tank 2-sewage water inlet pipe 21-wastewater influent tube valve 3-back flushing water inlet pipe
31-back flushing water inlet pipe valve 4-back flushing inlet pipe 41-back flushing inlet pipe valve
42-gas meter 5-sludge pump 6-aeration tube 7-water purifying tank
8-overfalling weir 9-hydraulic pipe 10-inhalant region 11-baffle plate
12-filtrating area 121-dividing plate 122-through hole 123-filter
Embodiment
For making the purpose of this utility model, technical scheme and advantage clearly, below in conjunction with accompanying drawing, the utility model is described in further detail.Except the arrow be connected with mark, the solid arrow in accompanying drawing is designated as water (flow) direction.
As shown in Figure 1, a kind of upward flowing type BAF, comprise 3 filter tanks of connecting successively 1, except first filter tank 1, any one filter tank 1 is equipped with overfalling weir 8 at the top near side, upper level filter tank 1, and the inhalant region 10 in any one filter tank 1 is all connected by hydraulic pipe 9 with the overfalling weir 8 in this filter tank, the height of the overfalling weir 8 in these 3 filter tanks reduces to side, water side gradually from feed-water end side.Any one filter tank 1 is equipped with inhalant region 10 and filtrating area 12, and inhalant region 10 is arranged on the downside of filtrating area 12, and the lower end adjacent with inhalant region 10 of filtrating area 12 is provided with the support dividing plate 121 with filter 123; Inhalant region is connected with the shore pipe being provided with spoil disposal valve and sludge pump 5; Be abound with the biofilter material of haydite shape in filtrating area 12, biofilter material upper end is provided with the baffle plate 11 of band flowing hole; Wherein filter tank 1, baffle plate 11 are skeleton construction with dividing plate 121, and be also provided with aeration tube 6 in the filtrating area 12 in filter tank, aeration tube is provided with solarization air cap.
From sewage purification and blowdown process, working process of the present utility model is elaborated respectively below.
Sewage purification process
As shown in Figure 1, first enter sewage water inlet pipe 2 through pretreated sewage, and enter the inhalant region 10 bottom first filter tank 1, left side by wastewater influent tube valve 21, sewage enters filtrating area 12 by the filter 123 on support dividing plate 121 subsequently; Meanwhile, make gas enter filtrating area 12 by aeration tube 6 by air delivery pump in aerating apparatus, make the gas-water mixture after sewage and air mixed upwards enter filter material layer in filtrating area 12.
The biofilter material of the haydite shape evenly gathered in filter material layer is attached with microbial film, when the microbial film of sewage on biofilter material, in the filter material layer nearer apart with inhalant region 10, organic content in sewage is higher, various heterotrophic bacterium is preponderated, and because aerating system provides oxygen, now eliminate a large amount of organic pollutants; In the filter material layer nearer apart with baffle plate 11, the organic content in sewage is lower, and the nitrifier of autotrophic type will be preponderated, and now mainly carry out the nitration reaction of ammonia nitrogen; Nitrifier is present in inside microbial film, and filtrate has very strong sticking power, once be formed, not easily come off completely, therefore BAF has the ability of very strong nitrated removal ammonia nitrogen.In whole filtrating area 12, due in the filter material layer piled up and the inside of microbial film there is anaerobic environment, can achieve part denitrification while nitrated, the flowing hole of nitrogen directly on baffle plate 11 is also discharged from top, filter tank.
Along with the carrying out of filtering, the biomass newly produced due to filter material surface gets more and more, the ss suspended solid retained constantly increases, when solid matter accumulation acquires a certain degree, then pile up and form mud and to be retained in filtrating area 12 and to precipitate, only have the water after filtration by, process water after filtration enters the overfalling weir 8 in second filter tank, then hydraulic pipe 9 pipeline connected by overfalling weir 8 enters the inhalant region in this filter tank under the effect of self gravitation, after same treating processes, enter the 3rd filter tank again, the clean water finally obtained flows into water purifying tank 7.
Blowdown process
If when the mud in inhalant region 10 is more, closes the wastewater influent tube valve 21 on sewage water inlet pipe 2, open the spoil disposal valve on mud line, start sludge pump 5, after forcing the mud gathered in discharge inhalant region 10, then close spoil disposal valve, proceed sewage purification process.
The utility model also can set up back-purge system, as shown in Figure 2 (pipeline be connected with inhalant region, filter tank 10 except the first step in figure does not all draw, and does not draw part identical with the first step).Back-purge system comprises back flushing water inlet pipe 3 and back flushing inlet pipe 4, back flushing water inlet pipe 3 is connected with inhalant region 10 by the back flushing water inlet pipe valve 31 that it is arranged, back flushing inlet pipe 4 is connected with inhalant region 10 by the back flushing inlet pipe valve 41 that it is arranged, and back flushing water inlet pipe is in parallel with mud line, back flushing inlet pipe 4 is also provided with the gas meter 42 making the volume ratio of air input and flooding quantity be stabilized in 3:1.
Back-purge system can carry out following backwash process, and when the sludge quantity in filtrating area 12 reaches setting degree, can carry out back flushing to filtrating area 12 and recover detergent power to make filtrating area 12, back flushing generally has following two kinds of modes:
The first backwash mode
If when the mud in inhalant region 10 is more, close the wastewater influent tube valve 21 on sewage water inlet pipe 2 and aerating system, and the back flushing water inlet pipe valve 31 of closing in back flushing water inlet pipe 3 and back flushing inlet pipe 4 and back flushing inlet pipe valve 41, open the spoil disposal valve on mud line, start sludge pump 5, after forcing the mud gathered in discharge inhalant region 10, then close spoil disposal valve; Back flushing water inlet pipe 3 is connected with water purifying tank 7, then back flushing water inlet pipe valve 31 and back flushing inlet pipe valve 41 is opened, and be 3:1 by the ratio that the gas meter 42 in back flushing inlet pipe 4 controls back flushing air input and back flushing flooding quantity, air water upwards flows to filtrating area 12 from inhalant region by filter 123 jointly, and filter 123 is washed away, can effectively avoid filter to block.Sewage after back flushing comes back to pretreatment system and processes.
The second backwash mode
Close the wastewater influent tube valve 21 on sewage water inlet pipe 2 and aerating system, and the spoil disposal valve of closing on mud line, open the back flushing inlet pipe valve 41 in back flushing inlet pipe 4, first carry out gas punching separately through back flushing inlet pipe 4, then open back flushing water inlet pipe valve 31 and back flushing inlet pipe valve 41 simultaneously, and the volume ratio controlling air input and flooding quantity is at 3:1, air water is with upwards flowing to filtrating area 12 from inhalant region 10 by filter 123, and filter 123 is washed away, at air water under phase mutual friction between the fluid scouring of filtrate and filtrate, aging microbial film is separated with filtrate with the SS be trapped, the microbial film rinsed and SS discharge filter tank 1 by baffle plate 11 with back flushing draining, be back to pretreatment system, last back flushing water inlet pipe 3 of opening separately again carries out water rinse, recovers the processing power in filter tank 1.
Claims (3)
1. a upward flowing type BAF, it is characterized in that: this BAF comprises several filter tanks of connecting successively (1), in any one filter tank (1), be provided with filtrating area (12) and inhalant region (10) from top to bottom;
Described inhalant region (10) is connected with sewage water inlet pipe (2), sewage water inlet pipe (2) is provided with wastewater influent tube valve (21), described inhalant region (10) is also connected with shore pipe, and described mud line is provided with spoil disposal valve and sludge pump (5);
The biofilter material of haydite shape is abound with in described filtrating area (12), the downside of filtrating area (12) is provided with support dividing plate (121), dividing plate (121) is evenly equipped with the through hole (122) penetrating plate body, described through hole (122) place is installed with filter (123); This filter tank also in the upside of dividing plate (121), the downside of biofilter material is provided with aeration tube (6), the pipe shaft of described aeration tube (6) is provided with solarization air cap;
Except first filter tank (1), any one filter tank (1) is equipped with overfalling weir (8) at the top near upper level filter tank (1) side, and the inhalant region (10) of any one filter tank (1) is all connected by hydraulic pipe (9) with the overfalling weir (8) in this filter tank; The height of the overfalling weir (8) in this multiple filter tank reduces to side, water side gradually from feed-water end side.
2. a kind of upward flowing type BAF according to claim 1, is characterized in that: the upside of described filtrating area (12) is provided with baffle plate (11), and (11) offer flowing hole to described baffle plate.
3. a kind of upward flowing type BAF according to claim 1, is characterized in that: described filter tank (1), dividing plate (121) and baffle plate (11) are skeleton construction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420784793.6U CN204356134U (en) | 2014-12-11 | 2014-12-11 | A kind of upward flowing type BAF |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420784793.6U CN204356134U (en) | 2014-12-11 | 2014-12-11 | A kind of upward flowing type BAF |
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| Publication Number | Publication Date |
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| CN204356134U true CN204356134U (en) | 2015-05-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420784793.6U Active CN204356134U (en) | 2014-12-11 | 2014-12-11 | A kind of upward flowing type BAF |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104528922A (en) * | 2014-12-11 | 2015-04-22 | 安徽南风环境工程技术有限公司 | Upward flow type biological aerated filter |
| CN108328866A (en) * | 2018-02-27 | 2018-07-27 | 中国农业大学 | A kind of biogas slurry treatment system and method |
-
2014
- 2014-12-11 CN CN201420784793.6U patent/CN204356134U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104528922A (en) * | 2014-12-11 | 2015-04-22 | 安徽南风环境工程技术有限公司 | Upward flow type biological aerated filter |
| CN108328866A (en) * | 2018-02-27 | 2018-07-27 | 中国农业大学 | A kind of biogas slurry treatment system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Liu Cun Inventor after: Xiao Zhongxin Inventor after: Dong Qiang Inventor after: Liu Dongwei Inventor after: Zhu Rong Inventor after: Hu Fangmei Inventor after: Cao Wen Inventor before: Liu Cun Inventor before: Xiao Zhongxing Inventor before: Dong Qiang Inventor before: Liu Dongwei Inventor before: Zhu Rong Inventor before: Hu Fangmei Inventor before: Cao Wen |
|
| CB03 | Change of inventor or designer information |